JPH11114534A - Special fly ash treatment method - Google Patents
Special fly ash treatment methodInfo
- Publication number
- JPH11114534A JPH11114534A JP9285852A JP28585297A JPH11114534A JP H11114534 A JPH11114534 A JP H11114534A JP 9285852 A JP9285852 A JP 9285852A JP 28585297 A JP28585297 A JP 28585297A JP H11114534 A JPH11114534 A JP H11114534A
- Authority
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- Japan
- Prior art keywords
- fly ash
- heavy metals
- concentration
- liter
- weight
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Abstract
(57)【要約】
【課題】ごみ焼却場等で発生する飛灰のうち、従来の無
害化処理では十分に重金属を除去することができない特
殊飛灰(pH10.5〜12.7、アルカリ度1000
〜2200mg/L、アルミニウム含有量2重量%以上
の飛灰)に対して有効である、安全で確実、かつ、低コ
ストの重金属固定化方法を提供する。
【解決手段】上記特殊飛灰に40〜200℃、好ましく
は60〜120℃の加熱処理を施す工程と、炭酸塩、炭
酸水素塩または炭酸ガスを添加し混練する工程とを有
し、好ましくは、ジチオカルバミン酸系キレート剤等の
重金属固定処理剤を添加して混練する工程を有する重金
属固定化方法。(57) [Summary] Special fly ash (pH 10.5 to 12.7, alkalinity) which cannot sufficiently remove heavy metals by conventional detoxification treatment among fly ash generated in waste incineration plants and the like 1000
The present invention provides a safe, reliable, and low-cost method for immobilizing heavy metals, which is effective for 灰 2200 mg / L and fly ash having an aluminum content of 2% by weight or more. The method includes a step of subjecting the special fly ash to a heat treatment at 40 to 200 ° C., preferably 60 to 120 ° C., and a step of adding and kneading a carbonate, a hydrogen carbonate or a carbon dioxide gas. And a method for immobilizing heavy metals such as a dithiocarbamic acid-based chelating agent and kneading.
Description
【0001】[0001]
【発明の属する技術分野】本発明は、重金属固定剤に係
り、特に、pH10.5〜12.7、アルカリ度100
0〜2200mg/リットル、ブランクCa溶出濃度1
00〜6000mg/リットル、およびアルミニウム含
有量2重量%以上という、特殊な飛灰中の重金属固定化
方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heavy metal fixing agent, and more particularly, to a pH of 10.5 to 12.7 and an alkalinity of 100.
0-2200 mg / liter, blank Ca elution concentration 1
The present invention relates to a method for immobilizing heavy metals in fly ash having a specific content of 00 to 6000 mg / liter and an aluminum content of 2% by weight or more.
【0002】[0002]
【従来技術】従来、ごみ焼却場等において、焼却後に残
る灰から重金属が溶出し、二次公害が発生するおそれが
あるため、焼却飛灰等は、重金属キレート剤を添加し、
キレート化合物として重金属を固定化したり、セメント
等で安定化するなどの無害化処理が加えられている。2. Description of the Related Art Conventionally, heavy metals are eluted from ash remaining after incineration in a garbage incineration plant or the like, and secondary pollution may occur.
Detoxification treatments such as fixing a heavy metal as a chelate compound or stabilizing with a cement or the like have been added.
【0003】[0003]
【発明が解決しようとする課題】しかし、飛灰の中に
は、上記の重金属の無害化処理では不十分なものも多
い。例えば、pHが変動しやすく、それに伴いPbイオ
ンの溶出量が不安定で、キレート剤を添加すると逆に重
金属の溶出量を増大させたりする一連の特殊飛灰があ
る。従来、これら特殊飛灰は処理結果からしか判別する
ことができず、かかる特殊飛灰を発生しやすい焼却場飛
灰の無害化処理対策は、非常に困難であった。However, among the fly ash, there are many fly ash in which the detoxification treatment of heavy metals is not sufficient. For example, there is a series of special fly ash in which the pH easily fluctuates, the elution amount of Pb ions is unstable, and the addition of a chelating agent increases the elution amount of heavy metals. Conventionally, these special fly ash can be distinguished only from the processing results, and it has been extremely difficult to take measures to detoxify the incineration fly ash, which tends to generate such special fly ash.
【0004】本発明者らは、鋭意探索の結果、これらの
特殊飛灰は、pH10.5〜12.7、アルカリ度10
00〜2200mg/リットル、ブランクCa溶出濃度
100〜6000mg/リットル、およびアルミニウム
含有量2重量%以上の飛灰であることを見いだした。The present inventors have conducted intensive searches and found that these special fly ash have a pH of 10.5 to 12.7 and an alkalinity of 10
It was found that the fly ash had a concentration of 00 to 2200 mg / liter, a blank Ca elution concentration of 100 to 6000 mg / liter, and an aluminum content of 2% by weight or more.
【0005】かかる特殊飛灰が特異な挙動を示す要因
は、飛灰中に含まれるアルミニウムイオンが水和反応す
るためと考えられているが、カルシウムイオンが系内に
多く存在している場合には、その緩衝作用でpHが安定
し、重金属溶出量の安定した飛灰となり、処理も容易な
ものになる。It is believed that the special behavior of such special fly ash is due to the hydration reaction of aluminum ions contained in the fly ash. Has a stable pH due to its buffering action, becomes fly ash with a stable elution amount of heavy metals, and is easy to treat.
【0006】本発明は、以上のような事情に鑑みてなさ
れたものであり、上記特殊飛灰に対して、安全で確実、
かつ、低コストの重金属固定化方法を提供することを目
的とする。The present invention has been made in view of the above-described circumstances, and is safe and reliable for the above-mentioned special fly ash.
Another object of the present invention is to provide a low-cost method for fixing heavy metals.
【0007】[0007]
【課題を解決するための手段】本発明の対象は、そのp
H、アルカリ度、ブランクCa溶出濃度およびアルミニ
ウム含有量が特定範囲に含まれる特殊飛灰である。SUMMARY OF THE INVENTION The object of the present invention is that
It is a special fly ash whose H, alkalinity, blank Ca elution concentration and aluminum content are included in specific ranges.
【0008】本発明の処理対象となる飛灰中のpHは、
飛灰50gを500mLの水と共に1LのPP容器に入
れ、振巾5cm、200回転/分の振盪器で20℃室温
6時間振盪後、孔径1μmのグラスフィルターで吸引濾
別して濾液を得る、環境庁告示13号法で定められた方
法により得られた濾液について、pHメーターで測定し
た。The pH in the fly ash to be treated according to the present invention is as follows:
50 g of fly ash is placed in a 1 L PP container together with 500 mL of water, shaken at 5 ° C., 200 rpm at room temperature for 6 hours with a shaker at 200 rpm, and filtered by suction with a glass filter having a pore size of 1 μm to obtain a filtrate. The filtrate obtained by the method specified in Notification No. 13 was measured with a pH meter.
【0009】上記アルカリ度は、環境庁告示13号で定
められた上記溶出テスト方法による飛灰溶出液を中和す
るに要する炭酸ナトリウム消費量(mg/リットル)を
中和滴定で測定した。The alkalinity was measured by neutralization titration of sodium carbonate consumption (mg / liter) required to neutralize the fly ash eluate according to the elution test method specified by the Environment Agency Notification No. 13.
【0010】ブランクCa溶出濃度は、上記飛灰溶出液
について、誘導結合高周波プラズマ分光分析(ICP)
で測定した。The concentration of the eluted blank Ca is determined by inductively coupled high frequency plasma spectroscopy (ICP) of the above fly ash eluate.
Was measured.
【0011】また、アルミニウム含有量は、飛灰1.0
gを2.0gの熱濃塩酸に溶解希釈して、ブランクCa
濃度と同様にICPによって濃度を測定した。The aluminum content is 1.0% fly ash.
g was dissolved and diluted in 2.0 g of hot concentrated hydrochloric acid.
The concentration was measured by ICP in the same manner as the concentration.
【0012】以上のような物性値で特定される飛灰は、
pH値が変動しやすく、それに伴いPbイオンの溶出量
が不安定で、キレート剤を添加すると逆に重金属の溶出
量を増大させたりする特殊性を有する。Fly ash specified by the above physical properties is
The pH value is liable to fluctuate, and the elution amount of Pb ions is unstable, and the addition of a chelating agent conversely increases the elution amount of heavy metals.
【0013】本発明の飛灰処理方法は、かかる特殊飛灰
に、水、炭酸塩、炭酸水素塩を、またはそれら塩の水溶
液を添加し、混練する工程を有すること、またはかかる
特殊飛灰に、水を添加、混練後に炭酸ガスを接触させる
工程を有することを特徴とする。[0013] The fly ash treatment method of the present invention comprises a step of adding water, carbonate, bicarbonate, or an aqueous solution of such a salt to the special fly ash and kneading it, or , Water and kneading after kneading.
【0014】好ましくは、前記混練時にジチオカルバミ
ン酸塩等の化合物を添加することを特徴とする。さらに
好ましくは、前記混練物を40〜200℃、好ましくは
60〜120℃に加熱処理することを特徴とする。Preferably, a compound such as dithiocarbamate is added during the kneading. More preferably, the kneaded material is heat-treated at 40 to 200C, preferably 60 to 120C.
【0015】[0015]
【発明の実施の形態】以下、本発明を詳細に説明する。
本発明では、かかる特殊飛灰に水を、飛灰100gに対
して20〜50g程度添加し、飛灰100gに対して1
〜20g、好ましくは1〜10g程度の炭酸塩若しくは
炭酸水素塩、または飛灰100gに対し0.1〜1リッ
トルの炭酸ガスを添加、混練を行う。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail.
In the present invention, water is added to such special fly ash in an amount of about 20 to 50 g per 100 g of fly ash, and 1 to 100 g of fly ash.
Carbon dioxide or bicarbonate of about 20 g, preferably about 1 to 10 g, or 0.1 g to 1 g of carbon dioxide gas is added to 100 g of fly ash and kneaded.
【0016】上記炭酸塩としては、炭酸ナトリウム、炭
酸カリウム等を、炭酸水素塩としては、炭酸水素ナトリ
ウム、炭酸水素カリウム等を例示することができる。こ
れらの内、コスト等の点から、炭酸ナトリウム、炭酸水
素ナトリウムの添加が特に好ましい。Examples of the carbonate include sodium carbonate and potassium carbonate, and examples of the hydrogen carbonate include sodium hydrogen carbonate and potassium hydrogen carbonate. Of these, addition of sodium carbonate and sodium hydrogencarbonate is particularly preferred from the viewpoint of cost and the like.
【0017】本発明においては、上記添加・混練処理時
に、ジチオカルバミン酸系キレート剤を添加、混練する
ことも好ましい。該キレート剤の併用効果は、前記特殊
飛灰の重金属の固定を助けるだけでなく、pHの変動の
大きい実際のゴミ焼却場の飛灰において、本発明の対象
とする以外の飛灰からの重金属溶出を防止するのに有効
である。In the present invention, it is also preferable to add and knead a dithiocarbamic acid-based chelating agent during the above addition / kneading treatment. The combined effect of the chelating agent not only helps fix the heavy metal in the special fly ash, but also in the fly ash of an actual garbage incineration plant having a large pH fluctuation, the heavy metal from the fly ash other than the object of the present invention. It is effective to prevent elution.
【0018】前記ジチオカルバミン酸系キレート剤とし
ては、例えば、ジエチルジチオカルバミン酸ナトリウ
ム、ジエチルジチオカルバミン酸カリウム等のジアルキ
ルジチオカルバミン酸塩、N,N’,N”−トリス(ジ
チオカルボキシ)ジエチレントリアミンナトリウム、
N,N’−ビス(ジチオカルボキシ)ジエチレントリア
ミン塩等の分子内にジチオカルバモイル基(N−C(=
S)S)を有する化合物を挙げることができる。Examples of the dithiocarbamic acid-based chelating agent include dialkyldithiocarbamates such as sodium diethyldithiocarbamate and potassium diethyldithiocarbamate; sodium N, N ', N "-tris (dithiocarboxy) diethylenetriamine;
In a molecule such as N, N'-bis (dithiocarboxy) diethylenetriamine salt, a dithiocarbamoyl group (NC (=
S) Compounds having S) can be mentioned.
【0019】前記ジチオカルバミン酸系キレート剤の添
加量は、飛灰100gに対し、0.1〜5gが好まし
い。また、本発明においては、飛灰の固化を目的として
セメントを添加することもできる。The amount of the dithiocarbamic acid-based chelating agent is preferably 0.1 to 5 g per 100 g of fly ash. In the present invention, cement can be added for the purpose of solidifying fly ash.
【0020】上記の混練物に加熱処理を施すとさらに固
定化効果が向上する。すなわち、40〜200℃、好ま
しくは60〜120℃の加熱処理を施す。加熱処理が4
0℃より低い場合には、固定化効果は悪くなる。逆に2
00℃よりも高くなると、固定化効果はあるが実用的で
はない。When the above kneaded material is subjected to a heat treatment, the fixing effect is further improved. That is, a heat treatment at 40 to 200 ° C, preferably 60 to 120 ° C is performed. 4 heat treatments
If the temperature is lower than 0 ° C., the immobilization effect will be poor. Conversely 2
If the temperature is higher than 00 ° C., there is an immobilization effect, but it is not practical.
【0021】[0021]
【実施例】以下、本発明を、実施例により更に詳細に説
明する。 (実施例1)A飛灰(本発明の対象特殊飛灰:表1に組
成分析値を示す。)100g、炭酸ナトリウム5.0
g、及び水40gをホバートミキサーに入れ、3分間攪
拌して餅状の混練物を得た。これをポリカップに入れて
1週間養生後、環境庁告示13号法の溶出試験法に従っ
て溶出液を得た。溶出液はpH11.7、Pb濃度0.
29mg/Lであった。The present invention will be described in more detail with reference to the following examples. (Example 1) 100 g of A fly ash (special fly ash subject to the present invention: the composition analysis value is shown in Table 1), sodium carbonate 5.0
g and 40 g of water were put into a Hobart mixer and stirred for 3 minutes to obtain a kneaded mixture. This was put in a polycup and cured for one week, and then an eluate was obtained according to the dissolution test method of No. 13 of the Notification of the Environment Agency. The eluate had a pH of 11.7 and a Pb concentration of 0.
It was 29 mg / L.
【0022】(比較例1)A飛灰100g、及び水40
gをホバートミキサーに入れ、3分間攪拌して餅状の混
練物を得た。これをポリカップに入れて1週間養生後、
環境庁告示13号法の溶出試験法に従って溶出液を得
た。溶出液はpH12.1、Pb濃度14mg/Lであ
った。実施例1と比較すると、A飛灰において、炭酸ナ
トリウム5.0gを添加することにより、Pb濃度が著
しく減少することがわかる。Comparative Example 1 A fly ash 100 g and water 40
g was put into a Hobart mixer and stirred for 3 minutes to obtain a kneaded mixture. After putting this in a polycup for one week,
An eluate was obtained according to the dissolution test method of the Environmental Agency Notification No. 13. The eluate had a pH of 12.1 and a Pb concentration of 14 mg / L. In comparison with Example 1, it can be seen that the addition of 5.0 g of sodium carbonate in the fly ash A significantly reduces the Pb concentration.
【0023】(実施例2)A飛灰100g、及び水40
gをホバートミキサーに入れ、2分間攪拌して細顆粒状
の混練物を得た。これをポリ袋に入れてヒートシール
し、0.75Lの炭酸ガスを注入したところ、炭酸ガス
は1〜2分で吸収された。ヒートシールしたまま1週間
養生させた後、環境庁告示13号法の溶出試験法に従っ
て溶出液を得た。溶出液はpH9.9、Pb濃度0.0
2mg/Lであった。比較例1と比較すると、A飛灰に
おいて、炭酸ガス0.75Lを注入することにより、p
H及びPb濃度が著しく減少することがわかる。Example 2 A fly ash 100 g and water 40
g was placed in a Hobart mixer and stirred for 2 minutes to obtain a fine granular kneaded product. This was put in a plastic bag, heat-sealed, and 0.75 L of carbon dioxide gas was injected. As a result, the carbon dioxide gas was absorbed in 1 to 2 minutes. After aging for one week with heat sealing, an eluate was obtained according to the dissolution test method of No. 13 of the Notification of the Environment Agency. The eluate was pH 9.9, Pb concentration 0.0
It was 2 mg / L. Compared with Comparative Example 1, by injecting 0.75 L of carbon dioxide gas into A fly ash,
It can be seen that the H and Pb concentrations are significantly reduced.
【0024】(実施例3)A飛灰100g、炭酸ナトリ
ウム5.0g、及びN,N’,N”−トリス(ジチオカ
ルボキシ)ジエチレントリアミンナトリウムを37%含
有する水溶液(以下、キレート剤Sとする。)2.0g
を、水40gに希釈した水溶液をホバートミキサーに入
れ、3分間攪拌して餅状の混練物を得た。これをポリカ
ップに入れて1週間養生後、環境庁告示13号法の溶出
試験法に従って溶出液を得た。溶出液はpH11.4、
Pb濃度<0.01mg/Lであった。実施例1と比較
すると、炭酸ナトリウムに加えてキレート剤Sを併用す
ることにより、Pbをほぼ除去できることがわかる。Example 3 An aqueous solution containing 100 g of fly ash A, 5.0 g of sodium carbonate, and 37% of sodium N, N ', N "-tris (dithiocarboxy) diethylenetriamine (hereinafter referred to as chelating agent S). ) 2.0g
Was added to a Hobart mixer and an aqueous solution diluted with 40 g of water was stirred for 3 minutes to obtain a rice cake-like kneaded product. This was put in a polycup and cured for one week, and then an eluate was obtained according to the dissolution test method of No. 13 of the Notification of the Environment Agency. The eluate was pH 11.4,
The Pb concentration was <0.01 mg / L. In comparison with Example 1, it is understood that Pb can be substantially removed by using the chelating agent S in addition to sodium carbonate.
【0025】(比較例2)A飛灰100g、キレート剤
S3.0g及び水40gをホバートミキサーに入れ、3
分間攪拌して餅状の混練物を得た。これをポリカップに
入れて1週間養生後、環境庁告示13号法の溶出試験法
に従って溶出液を得た。溶出液はpH12.1、Pb濃
度13mg/Lで、比較例2に示すように、炭酸ナトリ
ウムが存在せず、キレート剤Sのみを添加した場合に
は、室温で養生しただけではPbの固定は出来なかっ
た。Comparative Example 2 100 g of fly ash A, 3.0 g of chelating agent S and 40 g of water were put into a Hobart mixer and mixed.
After stirring for a minute, a kneaded product was obtained. This was put in a polycup and cured for one week, and then an eluate was obtained according to the dissolution test method of No. 13 of the Notification of the Environment Agency. The eluate had a pH of 12.1 and a Pb concentration of 13 mg / L. As shown in Comparative Example 2, when sodium carbonate was not present and only chelating agent S was added, Pb was immobilized only by curing at room temperature. I could not do it.
【0026】(実施例4)A飛灰100g、炭酸ナトリ
ウム5.0g及び水40gをホバートミキサーに入れ、
3分間攪拌して餅状の混練物を得た。これをポリカップ
に入れて80℃3時間加温処理をし、1週間養生後、環
境庁告示13号法の溶出試験法に従って溶出液を得た。
溶出液はpH11.7、Pb濃度0.1mg/Lであっ
た。Example 4 100 g of fly ash A, 5.0 g of sodium carbonate and 40 g of water were put into a Hobart mixer.
The mixture was stirred for 3 minutes to obtain a kneaded mixture. This was put in a polycup and heated at 80 ° C. for 3 hours. After curing for one week, an eluate was obtained according to the dissolution test method of the Environmental Agency Notification No. 13 method.
The eluate had a pH of 11.7 and a Pb concentration of 0.1 mg / L.
【0027】(比較例3)B飛灰(本発明の対象外飛
灰:表1に組成分析値を示す。)100g、及び水46
gをホバートミキサーに入れ、3分間攪拌して餅状の混
練物を得た。これをポリカップに入れて1週間養生後、
環境庁告示13号法の溶出試験法に従って溶出液を得
た。溶出液はpH12.6、Pb濃度22mg/Lであ
った。(Comparative Example 3) Fly ash B (100 g of fly ash not subject to the present invention; the composition analysis value is shown in Table 1) and water 46
g was put into a Hobart mixer and stirred for 3 minutes to obtain a kneaded mixture. After putting this in a polycup for one week,
An eluate was obtained according to the dissolution test method of the Environmental Agency Notification No. 13. The eluate had a pH of 12.6 and a Pb concentration of 22 mg / L.
【0028】(比較例4・5)B飛灰100g、炭酸ナ
トリウム10g及び水46gをホバートミキサーに入
れ、3分間攪拌して餅状の混練物を得た。これを2分し
て、それぞれポリ袋に入れ、一方を比較例4とした。他
方は80℃3時間加温処理をして比較例5とした。両試
料を1週間養生後、環境庁告示13号法の溶出試験法に
従って溶出液を得た。比較例4の溶出液はpH12.
6、Pb濃度5.6mg/Lで、比較例5の溶出液はp
H12.5、Pb濃度5.4mg/Lであった。B飛灰
では、A飛灰でみられたような、Pb濃度に対する炭酸
ナトリウムの十分な効果はみられなかった。(Comparative Examples 4.5) 100 g of fly ash B, 10 g of sodium carbonate and 46 g of water were put into a Hobart mixer and stirred for 3 minutes to obtain a cake-like kneaded product. This was divided into two parts, each of which was placed in a plastic bag. The other was heated at 80 ° C. for 3 hours to obtain Comparative Example 5. After curing both samples for one week, eluates were obtained in accordance with the dissolution test method of No. 13 of the Notification of the Environment Agency. The eluate of Comparative Example 4 was pH12.
6. When the Pb concentration was 5.6 mg / L, the eluate of Comparative Example 5 was p
H12.5 and Pb concentration were 5.4 mg / L. B fly ash did not show a sufficient effect of sodium carbonate on Pb concentration, as was observed with A fly ash.
【0029】(比較例6)B飛灰100g、及び水46
gをホバートミキサーに入れ、2分間攪拌して細顆粒状
の混練物を得た。これをポリ袋に入れてヒートシール
し、5.0Lの炭酸ガスを注入したところ、炭酸ガスは
1〜2分で吸収された。ヒートシールしたまま1週間養
生させた後、環境庁告示13号法の溶出試験法に従って
溶出液を得た。溶出液はpH12.1、Pb濃度2.4
mg/Lであった。B飛灰では、A飛灰でみられたよう
な、Pb濃度に対する炭酸ガスの十分な効果はみられな
かった。Comparative Example 6 Fly ash 100 g and water 46
g was placed in a Hobart mixer and stirred for 2 minutes to obtain a fine granular kneaded product. This was put in a plastic bag, heat-sealed, and 5.0 L of carbon dioxide gas was injected. As a result, the carbon dioxide gas was absorbed in 1 to 2 minutes. After aging for one week with heat sealing, an eluate was obtained according to the dissolution test method of No. 13 of the Notification of the Environment Agency. The eluate has a pH of 12.1 and a Pb concentration of 2.4.
mg / L. In the fly ash B, a sufficient effect of carbon dioxide gas on the Pb concentration as in the fly ash A was not observed.
【0030】以上の実施例1〜4及び比較例1〜6に使
用したA飛灰とB飛灰の組成分析値を表1に、実施例1
〜4及び比較例1〜6の実験結果を表2に、それぞれま
とめて示す。Table 1 shows the compositional analysis values of fly ash A and fly ash used in Examples 1 to 4 and Comparative Examples 1 to 6 described above.
Table 2 collectively shows the experimental results of Comparative Examples 1 to 4 and Comparative Examples 1 to 6.
【0031】[0031]
【表1】 [Table 1]
【0032】[0032]
【表2】 [Table 2]
【0033】[0033]
【発明の効果】以上の説明のように、本発明は、従来の
処理方法によっては、飛灰中の重金属を十分に無害化で
きないような組成の特殊飛灰に対して、有効な無害化処
理方法を提供するものである。本発明の処理方法は、安
全で容易かつ低コストの重金属固定化方法であり、特
に、前記特殊飛灰を発生しやすい焼却場における飛灰の
無害化処理等に有用である。As described above, the present invention provides an effective detoxifying treatment for a special fly ash having a composition that cannot sufficiently detoxify heavy metals in fly ash by the conventional treatment method. It provides a method. The treatment method of the present invention is a safe, easy and low-cost method for fixing heavy metals, and is particularly useful for detoxifying fly ash in incineration plants where special fly ash is likely to be generated.
Claims (10)
00〜2200mg/リットル、ブランクCa溶出濃度
100〜6000mg/リットル、およびアルミニウム
含有量2重量%以上の飛灰中の重金属固定化方法であっ
て、 炭酸塩若しくは炭酸水素塩を、飛灰に対して、1〜20
重量%添加し、混練する工程を有する、 飛灰中の重金属固定化処理方法。(1) pH: 10.5 to 12.7, alkalinity: 10
A heavy metal immobilization method in fly ash having a concentration of 100 to 2200 mg / liter, a blank Ca elution concentration of 100 to 6000 mg / liter, and an aluminum content of 2% by weight or more. , 1-20
A method for immobilizing heavy metals in fly ash, comprising a step of adding and mixing by weight.
00〜2200mg/リットル、ブランクCa溶出濃度
100〜6000mg/リットル、およびアルミニウム
含有量2重量%以上の飛灰中の重金属固定化方法であっ
て、 該飛灰に、炭酸塩若しくは炭酸水素塩を、飛灰に対し
て、1〜20重量%添加し、混練する工程と、 該混練物に、40〜200℃の加熱処理を施す工程とを
有する、 飛灰中の重金属固定化処理方法。2. A pH of 10.5 to 12.7 and an alkalinity of 10
A method for immobilizing heavy metals in fly ash having a concentration of 00 to 2200 mg / liter, a blank Ca elution concentration of 100 to 6000 mg / liter, and an aluminum content of 2% by weight or more, wherein a carbonate or bicarbonate is added to the fly ash. A method for immobilizing heavy metals in fly ash, comprising: adding 1 to 20% by weight to fly ash and kneading the mixture; and subjecting the kneaded material to a heat treatment at 40 to 200 ° C.
00〜2200mg/リットル、ブランクCa溶出濃度
100〜6000mg/リットル、およびアルミニウム
含有量2重量%以上の飛灰中の重金属固定化方法であっ
て、 炭酸ガスを、飛灰100gに対し、0.1〜1リットル
添加し、混練する工程を有する、 飛灰中の重金属固定化処理方法。3. A pH of 10.5 to 12.7 and an alkalinity of 10
A method for immobilizing heavy metals in fly ash having a concentration of 00 to 2200 mg / l, a blank Ca elution concentration of 100 to 6000 mg / l, and an aluminum content of 2% by weight or more, wherein carbon dioxide gas is added in an amount of 0.1 to 100 g of fly ash. A method for immobilizing heavy metals in fly ash, comprising a step of adding and mixing 1 to 1 liter.
00〜2200mg/リットル、ブランクCa溶出濃度
100〜6000mg/リットル、およびアルミニウム
含有量2重量%以上の飛灰中の重金属固定化方法であっ
て、 該飛灰に、炭酸ガスを、飛灰100gに対し、0.1〜
1リットル添加し、混練する工程と、 該混練物に、40〜200℃の加熱処理を施す工程とを
有する、 飛灰中の重金属固定化処理方法。4. pH 10.5-12.7, alkalinity 10
A method for immobilizing heavy metals in fly ash having a concentration of 00 to 2200 mg / l, a blank Ca elution concentration of 100 to 6000 mg / l, and an aluminum content of 2% by weight or more, wherein carbon dioxide gas is added to the fly ash and 100 g of fly ash is added. On the other hand, 0.1 ~
A method for immobilizing heavy metals in fly ash, comprising: adding 1 liter and kneading; and subjecting the kneaded material to a heat treatment at 40 to 200 ° C.
00〜2200mg/リットル、ブランクCa溶出濃度
100〜6000mg/リットル、およびアルミニウム
含有量2重量%以上の飛灰中の重金属固定化方法であっ
て、 該飛灰に、炭酸塩若しくは炭酸水素塩を、飛灰に対し
て、1〜20重量%添加する工程と、 ジチオカルバミン酸系キレート剤を、飛灰100gに対
し、0.1〜5g添加し、混練する工程とを有する、 飛灰中の重金属固定化処理方法。5. pH 10.5-12.7, alkalinity 10
A method for immobilizing heavy metals in fly ash having a concentration of 00 to 2200 mg / liter, a blank Ca elution concentration of 100 to 6000 mg / liter, and an aluminum content of 2% by weight or more, wherein a carbonate or bicarbonate is added to the fly ash. Fixing heavy metals in fly ash, comprising: adding 1 to 20% by weight to fly ash; and adding and kneading 0.1 to 5 g of a dithiocarbamic acid-based chelating agent to 100 g of fly ash. Treatment method.
00〜2200mg/リットル、ブランクCa溶出濃度
100〜6000mg/リットル、およびアルミニウム
含有量2重量%以上の飛灰中の重金属固定化方法であっ
て、 該飛灰に、炭酸塩若しくは炭酸水素塩を、飛灰に対し
て、1〜20重量%添加する工程と、 ジチオカルバミン酸系キレート剤を、飛灰100gに対
し、0.1〜5g添加し、混練する工程と、 該混練物に、40〜200℃の加熱処理を施す工程とを
有する、 飛灰中の重金属固定化処理方法。6. A pH of 10.5 to 12.7 and an alkalinity of 10
A method for immobilizing heavy metals in fly ash having a concentration of 00 to 2200 mg / liter, a blank Ca elution concentration of 100 to 6000 mg / liter, and an aluminum content of 2% by weight or more, wherein a carbonate or bicarbonate is added to the fly ash. A step of adding 1 to 20% by weight to the fly ash, a step of adding 0.1 to 5 g of a dithiocarbamic acid-based chelating agent to 100 g of the fly ash, and kneading; and a step of adding 40 to 200 to the kneaded material. A method of fixing heavy metals in fly ash.
00〜2200mg/リットル、ブランクCa溶出濃度
100〜6000mg/リットル、およびアルミニウム
含有量2重量%以上の飛灰中の重金属固定化方法であっ
て、 該飛灰に、炭酸ガスを、飛灰100gに対し、0.1〜
1リットル添加し、混練する工程と、 ジチオカルバミン酸系キレート剤を、飛灰100gに対
し、0.1〜5g添加し、混練する工程とを有する、 飛灰中の重金属固定化処理方法。7. pH 10.5-12.7, alkalinity 10
A method for immobilizing heavy metals in fly ash having a concentration of 00 to 2200 mg / l, a blank Ca elution concentration of 100 to 6000 mg / l, and an aluminum content of 2% by weight or more, wherein carbon dioxide gas is added to the fly ash and 100 g of fly ash is added. On the other hand, 0.1 ~
A method for immobilizing heavy metals in fly ash, comprising: adding 1 liter and kneading; and adding and kneading 0.1 to 5 g of a dithiocarbamic acid-based chelating agent to 100 g of fly ash.
00〜2200mg/リットル、ブランクCa溶出濃度
100〜6000mg/リットル、およびアルミニウム
含有量2重量%以上の飛灰中の重金属固定化方法であっ
て、 該飛灰に、炭酸ガスを、飛灰100gに対し、0.1〜
1リットル添加し、混練する工程と、 ジチオカルバミン酸系キレート剤を、飛灰100gに対
し、0.1〜5g添加し、混練する工程と、 該混練物に、40〜200℃の加熱処理を施す工程とを
有する、 飛灰中の重金属固定化処理方法。8. pH 10.5-12.7, alkalinity 10
A method for immobilizing heavy metals in fly ash having a concentration of 00 to 2200 mg / l, a blank Ca elution concentration of 100 to 6000 mg / l, and an aluminum content of 2% by weight or more, wherein carbon dioxide gas is added to the fly ash and 100 g of fly ash is added. On the other hand, 0.1 ~
Adding 1 liter and kneading; adding 0.1 to 5 g of a dithiocarbamic acid-based chelating agent to 100 g of fly ash; kneading; and subjecting the kneaded material to a heat treatment at 40 to 200 ° C. And a method for immobilizing heavy metals in fly ash.
処理方法。9. The method for immobilizing heavy metals according to claim 1, wherein the carbonate is sodium carbonate.
である、 請求項1、2、5、6のいずれかに記載の重金属固定化
処理方法。10. The method for immobilizing heavy metals according to claim 1, wherein the bicarbonate is sodium bicarbonate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP28585297A JP3949795B2 (en) | 1997-10-17 | 1997-10-17 | Special fly ash treatment method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP28585297A JP3949795B2 (en) | 1997-10-17 | 1997-10-17 | Special fly ash treatment method |
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| Publication Number | Publication Date |
|---|---|
| JPH11114534A true JPH11114534A (en) | 1999-04-27 |
| JP3949795B2 JP3949795B2 (en) | 2007-07-25 |
Family
ID=17696900
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP28585297A Expired - Fee Related JP3949795B2 (en) | 1997-10-17 | 1997-10-17 | Special fly ash treatment method |
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| Country | Link |
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| JP (1) | JP3949795B2 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005118617A (en) * | 2003-10-14 | 2005-05-12 | Nippon Soda Co Ltd | Method for immobilizing heavy metals in fly ash |
| JP2006281150A (en) * | 2005-04-04 | 2006-10-19 | Takuma Co Ltd | Garbage incinerator with incineration ash reformer |
| CN104607434A (en) * | 2015-02-10 | 2015-05-13 | 重庆大学 | Municipal solid waste incineration fly ash curing method |
| CN114538489A (en) * | 2022-03-18 | 2022-05-27 | 四川轻化工大学 | Method and system for preparing efficient powdery accelerator from aluminum ash |
-
1997
- 1997-10-17 JP JP28585297A patent/JP3949795B2/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005118617A (en) * | 2003-10-14 | 2005-05-12 | Nippon Soda Co Ltd | Method for immobilizing heavy metals in fly ash |
| JP2006281150A (en) * | 2005-04-04 | 2006-10-19 | Takuma Co Ltd | Garbage incinerator with incineration ash reformer |
| CN104607434A (en) * | 2015-02-10 | 2015-05-13 | 重庆大学 | Municipal solid waste incineration fly ash curing method |
| CN114538489A (en) * | 2022-03-18 | 2022-05-27 | 四川轻化工大学 | Method and system for preparing efficient powdery accelerator from aluminum ash |
| CN114538489B (en) * | 2022-03-18 | 2023-07-14 | 四川轻化工大学 | A method and system for preparing high-efficiency powder accelerator by using aluminum ash |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3949795B2 (en) | 2007-07-25 |
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